US9127097B2ActiveUtilityA1

P-N-P ligand

88
Assignee: NOVA CHEM INT SAPriority: Jan 25, 2012Filed: Apr 22, 2015Granted: Sep 8, 2015
Est. expiryJan 25, 2032(~5.6 yrs left)· nominal 20-yr term from priority
C07C 2531/14C07C 2531/34C08F 4/69B01J 2531/62B01J 2231/20C07F 9/4883C07C 2531/24C08F 10/02B01J 31/187C07F 9/5325C07C 2/36
88
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References
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Claims

Abstract

A new P-N-P ligand is useful in ethylene oligomerizations. In combination with i) a source of chromium; and ii) an activator such as methylalumoxane; the ligand of this invention may be used to prepare an oligomer product that contains a mixture of high purity alpha olefins. In a preferred embodiment, the ligand of this invention enables a selective oligomerization in which the majority of the liquid product is a mixture of hexene and octene. The amount of by-product polymer that is produced in preferred oligomerization reactions is advantageously low.

Claims

exact text as granted — not AI-modified
The invention claimed is: 
     
       1. A process for the oligomerization of ethylene, wherein said process comprises contacting ethylene under oligomerization conditions with a catalyst system comprising
 i) a source of chromium; 
 ii) a ligand defined by the formula 
 
       
         
           
           
               
               
           
         
         
           wherein Ar 1  is selected from the group consisting of aromatic hydrocarbyl and aromatic heterohydrocarbyl; Ar F  is an aromatic fluorocarbyl oxide; Ar 3  and Ar 4  are independently selected from the group consisting of aromatic hydrocarbyl, aromatic heterohydrocarbyl and aromatic fluorocarbyl oxide; and R 1  is selected from the group consisting of hydrocarbyl and heterohydrocarbyl; and 
         
         iii) an activator. 
       
     
     
       2. The process of  claim 1  when undertaken at a temperature of from about 10° C. to about 300° C. and a pressure of from about 5 atmospheres to about 150 atmospheres. 
     
     
       3. The process of  claim 1  wherein said source of Cr is selected from the group consisting of chromium chlorides, chromium carbonyl, chromium carboxylates and chromium acetylacetonate. 
     
     
       4. The process of  claim 1  wherein said activator comprises methylaluminoxane. 
     
     
       5. The process of  claim 1  which is further characterized by producing a liquid product stream which contains greater than about 25 weight % octene-1.

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